Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace
Preheating furnaces, which are commonly used in many production sectors (e.g., iron and steel), are simultaneously one of the most energy-intensive devices used in the industry. Partial replacement of natural gas with biomass-derived synthesis gas as a fuel used for heating would be an important ste...
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doaj-ac38634a768f41b6a4b8a068adb5d2b42020-11-25T02:33:57ZengMDPI AGEnergies1996-10732020-04-01131698169810.3390/en13071698Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating FurnacePiotr Jóźwiak0Jarosław Hercog1Aleksandra Kiedrzyńska2Krzysztof Badyda3Daniela Olevano4Thermal Processes Department, Institute of Power Engineering, 01-330 Warsaw, PolandThermal Processes Department, Institute of Power Engineering, 01-330 Warsaw, PolandThermal Processes Department, Institute of Power Engineering, 01-330 Warsaw, PolandInstitute of Heat Engineering, Warsaw University of Technology, 00-665 Warsaw, PolandCentro Sviluppo Materiali S.p.A., 00128 Rome, ItalyPreheating furnaces, which are commonly used in many production sectors (e.g., iron and steel), are simultaneously one of the most energy-intensive devices used in the industry. Partial replacement of natural gas with biomass-derived synthesis gas as a fuel used for heating would be an important step towards limiting industrial CO<sub>2</sub> emissions. The time dependent computational fluid dynamics (CFD) model of an exemplary furnace was created to evaluate whether it is possible to obtain 40% of energy from syngas combustion without deterioration of thermal parameters of the treated load. As an outcome, a promising method to organize co-firing in the furnace was indicated. The obtained results show that the co-firing method (up to 40% thermal natural gas replacement with syngas), assuming low air-to-fuel equivalence ratio (λ<sub>NG</sub> = 2.0) and even distribution of power among the furnace corners, lead to satisfactory efficiency of the heat treatment process—the heat transferred to the load exceeds 95% of the heat delivered to the load in the reference case), while carbon dioxide emission is reduced from 285.5 to 171.3 kg CO<sub>2</sub>/h. This study showed that it is feasible (from the heat transfer point of view) to decrease the environmental impact of the process industries by the use of renewable fuels.https://www.mdpi.com/1996-1073/13/7/1698CFD modellingheat treatment processindustrial furnacesnatural gas substitutionsyngas co-firing |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Piotr Jóźwiak Jarosław Hercog Aleksandra Kiedrzyńska Krzysztof Badyda Daniela Olevano |
spellingShingle |
Piotr Jóźwiak Jarosław Hercog Aleksandra Kiedrzyńska Krzysztof Badyda Daniela Olevano Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace Energies CFD modelling heat treatment process industrial furnaces natural gas substitution syngas co-firing |
author_facet |
Piotr Jóźwiak Jarosław Hercog Aleksandra Kiedrzyńska Krzysztof Badyda Daniela Olevano |
author_sort |
Piotr Jóźwiak |
title |
Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace |
title_short |
Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace |
title_full |
Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace |
title_fullStr |
Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace |
title_full_unstemmed |
Thermal Effects of Natural Gas and Syngas Co-Firing System on Heat Treatment Process in the Preheating Furnace |
title_sort |
thermal effects of natural gas and syngas co-firing system on heat treatment process in the preheating furnace |
publisher |
MDPI AG |
series |
Energies |
issn |
1996-1073 |
publishDate |
2020-04-01 |
description |
Preheating furnaces, which are commonly used in many production sectors (e.g., iron and steel), are simultaneously one of the most energy-intensive devices used in the industry. Partial replacement of natural gas with biomass-derived synthesis gas as a fuel used for heating would be an important step towards limiting industrial CO<sub>2</sub> emissions. The time dependent computational fluid dynamics (CFD) model of an exemplary furnace was created to evaluate whether it is possible to obtain 40% of energy from syngas combustion without deterioration of thermal parameters of the treated load. As an outcome, a promising method to organize co-firing in the furnace was indicated. The obtained results show that the co-firing method (up to 40% thermal natural gas replacement with syngas), assuming low air-to-fuel equivalence ratio (λ<sub>NG</sub> = 2.0) and even distribution of power among the furnace corners, lead to satisfactory efficiency of the heat treatment process—the heat transferred to the load exceeds 95% of the heat delivered to the load in the reference case), while carbon dioxide emission is reduced from 285.5 to 171.3 kg CO<sub>2</sub>/h. This study showed that it is feasible (from the heat transfer point of view) to decrease the environmental impact of the process industries by the use of renewable fuels. |
topic |
CFD modelling heat treatment process industrial furnaces natural gas substitution syngas co-firing |
url |
https://www.mdpi.com/1996-1073/13/7/1698 |
work_keys_str_mv |
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